JP6661005B2 - 平衡制限反応を転換する方法 - Google Patents
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- 238000006243 chemical reaction Methods 0.000 title claims description 63
- 239000002594 sorbent Substances 0.000 claims description 84
- 239000000463 material Substances 0.000 claims description 58
- 239000003054 catalyst Substances 0.000 claims description 55
- 239000000047 product Substances 0.000 claims description 36
- 239000007858 starting material Substances 0.000 claims description 36
- 238000000034 method Methods 0.000 claims description 21
- 239000007788 liquid Substances 0.000 claims description 20
- 238000000926 separation method Methods 0.000 claims description 10
- 239000002002 slurry Substances 0.000 claims description 10
- 230000003197 catalytic effect Effects 0.000 claims description 8
- 239000007795 chemical reaction product Substances 0.000 claims description 6
- 239000002608 ionic liquid Substances 0.000 claims description 5
- 239000007789 gas Substances 0.000 description 24
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 21
- 239000012071 phase Substances 0.000 description 18
- 239000007791 liquid phase Substances 0.000 description 7
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 6
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 5
- 239000003921 oil Substances 0.000 description 4
- 238000003786 synthesis reaction Methods 0.000 description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 4
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 3
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 3
- LYCAIKOWRPUZTN-UHFFFAOYSA-N Ethylene glycol Chemical compound OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 description 3
- 229910002092 carbon dioxide Inorganic materials 0.000 description 3
- 239000001569 carbon dioxide Substances 0.000 description 3
- 229910002091 carbon monoxide Inorganic materials 0.000 description 3
- 239000001257 hydrogen Substances 0.000 description 3
- 229910052739 hydrogen Inorganic materials 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- 239000008188 pellet Substances 0.000 description 3
- 239000007787 solid Substances 0.000 description 3
- 238000001179 sorption measurement Methods 0.000 description 3
- 238000003756 stirring Methods 0.000 description 3
- PUPZLCDOIYMWBV-UHFFFAOYSA-N (+/-)-1,3-Butanediol Chemical compound CC(O)CCO PUPZLCDOIYMWBV-UHFFFAOYSA-N 0.000 description 2
- ZXMGHDIOOHOAAE-UHFFFAOYSA-N 1,1,1-trifluoro-n-(trifluoromethylsulfonyl)methanesulfonamide Chemical compound FC(F)(F)S(=O)(=O)NS(=O)(=O)C(F)(F)F ZXMGHDIOOHOAAE-UHFFFAOYSA-N 0.000 description 2
- NJMWOUFKYKNWDW-UHFFFAOYSA-N 1-ethyl-3-methylimidazolium Chemical compound CCN1C=C[N+](C)=C1 NJMWOUFKYKNWDW-UHFFFAOYSA-N 0.000 description 2
- CRBJBYGJVIBWIY-UHFFFAOYSA-N 2-isopropylphenol Chemical compound CC(C)C1=CC=CC=C1O CRBJBYGJVIBWIY-UHFFFAOYSA-N 0.000 description 2
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 2
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- LCGLNKUTAGEVQW-UHFFFAOYSA-N Dimethyl ether Chemical compound COC LCGLNKUTAGEVQW-UHFFFAOYSA-N 0.000 description 2
- 241000196324 Embryophyta Species 0.000 description 2
- 239000003463 adsorbent Substances 0.000 description 2
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 239000006227 byproduct Substances 0.000 description 2
- TVZPLCNGKSPOJA-UHFFFAOYSA-N copper zinc Chemical compound [Cu].[Zn] TVZPLCNGKSPOJA-UHFFFAOYSA-N 0.000 description 2
- 238000009792 diffusion process Methods 0.000 description 2
- 239000011261 inert gas Substances 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- TZIHFWKZFHZASV-UHFFFAOYSA-N methyl formate Chemical compound COC=O TZIHFWKZFHZASV-UHFFFAOYSA-N 0.000 description 2
- 238000002156 mixing Methods 0.000 description 2
- 239000000843 powder Substances 0.000 description 2
- 238000010926 purge Methods 0.000 description 2
- 239000002904 solvent Substances 0.000 description 2
- 239000007921 spray Substances 0.000 description 2
- 230000035882 stress Effects 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- IQQRAVYLUAZUGX-UHFFFAOYSA-N 1-butyl-3-methylimidazolium Chemical compound CCCCN1C=C[N+](C)=C1 IQQRAVYLUAZUGX-UHFFFAOYSA-N 0.000 description 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- 241001507939 Cormus domestica Species 0.000 description 1
- 238000009620 Haber process Methods 0.000 description 1
- 238000005299 abrasion Methods 0.000 description 1
- 239000002250 absorbent Substances 0.000 description 1
- 230000002745 absorbent Effects 0.000 description 1
- 238000009825 accumulation Methods 0.000 description 1
- 230000002411 adverse Effects 0.000 description 1
- 229910021529 ammonia Inorganic materials 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 238000005243 fluidization Methods 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 239000002638 heterogeneous catalyst Substances 0.000 description 1
- 150000002431 hydrogen Chemical class 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 238000002955 isolation Methods 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 238000005580 one pot reaction Methods 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 238000005191 phase separation Methods 0.000 description 1
- 239000003495 polar organic solvent Substances 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 230000008092 positive effect Effects 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 230000008646 thermal stress Effects 0.000 description 1
- ZIBGPFATKBEMQZ-UHFFFAOYSA-N triethylene glycol Chemical compound OCCOCCOCCO ZIBGPFATKBEMQZ-UHFFFAOYSA-N 0.000 description 1
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- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
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- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/02—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds
- B01J8/0278—Feeding reactive fluids
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- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/005—Separating solid material from the gas/liquid stream
- B01J8/006—Separating solid material from the gas/liquid stream by filtration
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- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
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- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/005—Separating solid material from the gas/liquid stream
- B01J8/007—Separating solid material from the gas/liquid stream by sedimentation
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
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- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/18—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
- B01J8/20—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles with liquid as a fluidising medium
- B01J8/22—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles with liquid as a fluidising medium gas being introduced into the liquid
- B01J8/222—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles with liquid as a fluidising medium gas being introduced into the liquid in the presence of a rotating device only
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- B—PERFORMING OPERATIONS; TRANSPORTING
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- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/18—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
- B01J8/20—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles with liquid as a fluidising medium
- B01J8/22—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles with liquid as a fluidising medium gas being introduced into the liquid
- B01J8/224—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles with liquid as a fluidising medium gas being introduced into the liquid the particles being subject to a circulatory movement
- B01J8/228—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles with liquid as a fluidising medium gas being introduced into the liquid the particles being subject to a circulatory movement externally, i.e. the particles leaving the vessel and subsequently re-entering it
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- B—PERFORMING OPERATIONS; TRANSPORTING
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- B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
- B01J2208/00008—Controlling the process
- B01J2208/00017—Controlling the temperature
- B01J2208/00106—Controlling the temperature by indirect heat exchange
- B01J2208/00168—Controlling the temperature by indirect heat exchange with heat exchange elements outside the bed of solid particles
- B01J2208/00176—Controlling the temperature by indirect heat exchange with heat exchange elements outside the bed of solid particles outside the reactor
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- B01J2208/00017—Controlling the temperature
- B01J2208/00106—Controlling the temperature by indirect heat exchange
- B01J2208/00265—Part of all of the reactants being heated or cooled outside the reactor while recycling
- B01J2208/00283—Part of all of the reactants being heated or cooled outside the reactor while recycling involving reactant liquids
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
- B01J2208/00008—Controlling the process
- B01J2208/00017—Controlling the temperature
- B01J2208/00106—Controlling the temperature by indirect heat exchange
- B01J2208/00265—Part of all of the reactants being heated or cooled outside the reactor while recycling
- B01J2208/00292—Part of all of the reactants being heated or cooled outside the reactor while recycling involving reactant solids
- B01J2208/003—Part of all of the reactants being heated or cooled outside the reactor while recycling involving reactant solids involving reactant slurries
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- B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
- B01J2208/00796—Details of the reactor or of the particulate material
- B01J2208/00805—Details of the particulate material
- B01J2208/00814—Details of the particulate material the particulate material being provides in prefilled containers
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
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- B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
- B01J2208/00796—Details of the reactor or of the particulate material
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
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- B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
- B01J2208/00796—Details of the reactor or of the particulate material
- B01J2208/00893—Feeding means for the reactants
- B01J2208/00902—Nozzle-type feeding elements
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- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- Combustion & Propulsion (AREA)
- Physical Or Chemical Processes And Apparatus (AREA)
- Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
- Gas Separation By Absorption (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Description
CO2+3H2→CH3OH+H2O (式2)
この合成法の典型的な副生物は、水、ジメチルエーテル、蟻酸メチル及びエタノールである。工業的には、反応には、主として、銅−亜鉛酸化物−アルミナ触媒が用いられる。
1 反応装置
2 反応器
4 触媒材料
6 出発材料
8 生成物
10 収着剤
12 静穏化帯域又は反応帯域 集合帯域
14 相分離器
16 出発材料供給装置 気体供給装置
18 分離装置
19 バスケット
20 メッシュ
22 下部帯域
24 反応帯域
26 液相反応器 スラリー反応器
28 担体液体
32 スプレーノズル
34 撹拌装置
36、36’ 熱交換装置
38 パージ気体流
40 ポンプ
42 バルブ
44 固定床
Claims (11)
- −デッドエンド反応器である反応器(2)内に触媒材料(4)を配置する工程と、
−前記反応器(2)に出発材料(6)を導入する工程と、
−前記出発材料(6)を反応させて生成物(8)を形成する工程と、
−収着剤(10)を前記反応器(2)に導入する工程と、
−前記収着剤(10)により前記生成物(8)を収着させる工程と、
を有する平衡制約反応を転化させる方法であって、
前記生成物(8)が詰め込まれた前記収着剤(10)が前記反応器(2)内の収集帯域(12)に集められること、及び、前記触媒材料(4)が、前記収集帯域(12)から分離されるように、配置され、
前記生成物(8)が詰め込まれた前記収着剤(10)が、前記収集帯域(12)から相分離器(14)へ運ばれ、前記生成物(8)が、そこで前記収着剤(10)から分離され、
前記収着剤(10)が、前記反応器(2)へ/から連続的に導入および排出され、前記反応器(2)が、前記反応器(2)内のガス濃度を継続的に測定し、供給気体成分が枯渇した場合に、この気体成分を供給する、ことを特徴とする方法。 - 前記生成物(8)が圧力低下により前記収着剤(10)から分離されることを特徴とする請求項1に記載の方法。
- 前記生成物から分離された前記収着剤(10)が前記反応器(2)へ再循環されることを特徴とする請求項1または2に記載の方法。
- 前記出発材料(6)が反応器(2)内へ気体状で導入され、反応が気相で行なわれること及び前記収着剤(10)が分離装置(18)に収容された前記触媒材料(4)と接触しないやり方で前記反応器(2)に運搬されることを特徴とする請求項1〜3のいずれか1項に記載の方法。
- 前記収着剤がイオン性液体であることを特徴とする請求項1〜4のいずれか1項に記載の方法。
- デッドエンド反応器である反応器(2)及び前記反応器(2)に設置された出発材料入口装置(16)を含有し、更に前記反応器(2)内に配置された触媒材料(4)及び同様に前記反応器(2)内に存在して出発材料(6)からの反応で形成される生成物(8)を収着するための収着剤(10)を含有する平衡制約反応を転化するための反応装置であって、
収着剤収集帯域(12)が前記反応器(2)内に設けられ、前記触媒材料(4)を前記収集帯域から分離するための装置(18)が前記反応器(2)内に配置され、
前記生成物(8)が詰め込まれた収着剤(10)が、前記収集帯域(12)から相分離器(14)に運ばれ、前記生成物(8)が、そこで前記収着剤(10)から分離でき、
前記収着剤(10)が、前記反応器(2)へ/から連続的に導入および排出され、前記反応器(2)が、前記反応器(2)内のガス濃度を継続的に測定し、供給気体成分が枯渇した場合に、この気体成分を供給する、ことを特徴とする装置。 - 前記収集帯域(12)が前記反応器(2)の下部領域(22)に配置され、分離メッシュ(20)により前記反応器(2)の反応帯域(24)から分離されていることを特徴とする請求項6に記載の反応装置。
- 前記触媒材料(4)が反応帯域(24)において気体透過性又は液体透過性のバスケット(19)内に配置されていることを特徴とする請求項6に記載の反応装置。
- 前記反応器(2)が、その中に担体液体(28)を有するスラリー反応器(26)であることを特徴とする請求項6〜8のいずれか1項に記載の反応装置。
- 前記反応器(2)が固定床反応器(20)であることを特徴とする請求項6〜8のいずれか1項に記載の反応装置。
- 前記出発材料(6)を前記触媒材料(4)の間の隙間に分布させるためのファンが設けられていることを特徴とする請求項10に記載の反応装置。
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DE102015215662.1A DE102015215662A1 (de) | 2015-08-18 | 2015-08-18 | Verfahren zur Umsetzung von gleichgewichtslimitierten Reaktionen |
DE102015215662.1 | 2015-08-18 | ||
PCT/EP2016/066117 WO2017029024A1 (de) | 2015-08-18 | 2016-07-07 | Verfahren zur umsetzung von gleichgewichtslimitierten reaktionen |
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JP2018526203A JP2018526203A (ja) | 2018-09-13 |
JP6661005B2 true JP6661005B2 (ja) | 2020-03-11 |
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Country | Link |
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US (1) | US10618021B2 (ja) |
EP (1) | EP3313564A1 (ja) |
JP (1) | JP6661005B2 (ja) |
KR (1) | KR102116731B1 (ja) |
CN (1) | CN107921395B (ja) |
AU (1) | AU2016309524B2 (ja) |
CL (1) | CL2018000369A1 (ja) |
DE (1) | DE102015215662A1 (ja) |
MA (1) | MA42252A (ja) |
MX (1) | MX2018002024A (ja) |
SA (1) | SA518390908B1 (ja) |
TN (1) | TN2018000053A1 (ja) |
WO (1) | WO2017029024A1 (ja) |
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Publication number | Priority date | Publication date | Assignee | Title |
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DE102015215662A1 (de) | 2015-08-18 | 2017-02-23 | Friedrich-Alexander-Universität Erlangen-Nürnberg | Verfahren zur Umsetzung von gleichgewichtslimitierten Reaktionen |
DE102016204719A1 (de) * | 2016-03-22 | 2017-09-28 | Siemens Aktiengesellschaft | Reaktor |
DE102017204226A1 (de) * | 2017-03-14 | 2018-09-20 | Friedrich-Alexander-Universität Erlangen-Nürnberg | Mischung zur Verwendung als flüssiges Sorptionsmittel bei der Methanol-Synthese und Verfahren zur Methanol-Synthese unter Verwendung der Mischung |
DE102017206763A1 (de) * | 2017-04-21 | 2018-10-25 | Siemens Aktiengesellschaft | Verfahren und Vorrichtung zum Umsetzen von Kohlenstoffdioxid zu Methanol |
DK3556451T3 (da) * | 2018-04-20 | 2020-08-31 | Siemens Ag | Fremgangsmåde til drift af et reaktoranlæg |
EP3673967A1 (en) * | 2018-12-27 | 2020-07-01 | Vito NV | A device and method for separating at least one compound and at least one further compound contained in a fluidic mixture |
WO2022258779A1 (en) * | 2021-06-10 | 2022-12-15 | Universiteit Antwerpen | Device and process set-up for equilibrium reactions |
EP4230287A1 (en) * | 2022-02-16 | 2023-08-23 | Eidgenössische Materialprüfungs- und Forschungsanstalt | Sorption-enhanced catalytic reactors with thermal moderators |
Family Cites Families (22)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB2293334A (en) | 1994-09-26 | 1996-03-27 | Shell Int Research Maatschappij B V | Process for carrying out chemical equilibrium reactions |
EP0737646B1 (en) * | 1995-04-10 | 2000-09-06 | Air Products And Chemicals, Inc. | Process for operating equilibrium-controlled reactions |
US6303092B1 (en) | 1995-04-10 | 2001-10-16 | Air Products And Chemicals, Inc. | Process for operating equilibrium controlled reactions |
NL1003026C2 (nl) * | 1996-05-03 | 1997-11-06 | Tno | Reactor voor het uitvoeren van gasfase/vloeistoffase/vaste fase reacties, alsmede een werkwijze voor het uitvoeren van dergelijke reacties onder toepassing van deze reactor. |
JP2003221355A (ja) | 2002-01-25 | 2003-08-05 | Maruzen Petrochem Co Ltd | 環状ジアルデヒドの製造方法 |
US6969505B2 (en) * | 2002-08-15 | 2005-11-29 | Velocys, Inc. | Process for conducting an equilibrium limited chemical reaction in a single stage process channel |
US20040178124A1 (en) | 2003-03-11 | 2004-09-16 | Ke Liu | Hydrogen desulfurizer for hydrocarbon feeds with separated adsorption and catalyst material |
JP2005015294A (ja) * | 2003-06-27 | 2005-01-20 | Toshiba Corp | 化学反応装置 |
DE10361071A1 (de) | 2003-12-22 | 2005-07-14 | Basf Ag | Nitrilhydrierung in Gegenwart Ionischer Flüssigkeiten |
DE102004008575A1 (de) * | 2004-02-19 | 2005-09-08 | Stockhausen Gmbh | Spaltung oligomerer (Meth)acrylsäure in flüssiger Phase unter Druck |
US20050229490A1 (en) * | 2004-04-19 | 2005-10-20 | Texaco Inc. | Reactor and apparatus for hydrogen generation |
JP2005314500A (ja) | 2004-04-28 | 2005-11-10 | Mitsubishi Materials Corp | 高オクタン価ガソリン基材の製造方法 |
AU2009233786B2 (en) * | 2008-04-09 | 2014-04-24 | Velocys Inc. | Process for converting a carbonaceous material to methane, methanol and/or dimethyl ether using microchannel process technology |
US20120029245A1 (en) * | 2009-03-17 | 2012-02-02 | Oberon Fuels, Inc. | Catalytic reactions using ionic liquids |
CN102395527A (zh) * | 2009-03-27 | 2012-03-28 | 索尔维公司 | 生产过氧化氢的方法 |
CL2010000726A1 (es) | 2010-07-07 | 2010-12-24 | Haldor Topsoe As | Metodo para preparar metanol que comprende hacer reaccionar un gas de sintesis en un reactor catalitico de lecho fijo de particulas de catalizador enfriadas indirectamente, y condensar metanol a medida que se forma sobre una superficie de enfriamiento; y reactor para realizar dicho metodo. |
TWI428184B (zh) * | 2010-08-26 | 2014-03-01 | Atomic Energy Council | 提升漿態床反應器產率之方法 |
CN102371136B (zh) * | 2010-12-08 | 2013-10-09 | 北京低碳清洁能源研究所 | 生产富含ch4气体的具有同轴闭合夹层结构的反应器系统以及使用该系统的方法 |
EP2780283A4 (en) | 2011-11-14 | 2015-12-30 | Sitec Gmbh | METHOD AND SYSTEMS FOR METABOLIC TRICHLORINE PRODUCTION |
JP6116383B2 (ja) | 2013-05-31 | 2017-04-19 | ユニ・チャーム株式会社 | 吸収性物品 |
CN105175208B (zh) * | 2015-08-07 | 2017-11-14 | 北京华福工程有限公司 | 乙炔加氢制备乙烯的方法及用于该方法的反应塔 |
DE102015215662A1 (de) | 2015-08-18 | 2017-02-23 | Friedrich-Alexander-Universität Erlangen-Nürnberg | Verfahren zur Umsetzung von gleichgewichtslimitierten Reaktionen |
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MX2018002024A (es) | 2018-04-13 |
WO2017029024A1 (de) | 2017-02-23 |
TN2018000053A1 (en) | 2019-07-08 |
JP2018526203A (ja) | 2018-09-13 |
KR20180039717A (ko) | 2018-04-18 |
CL2018000369A1 (es) | 2018-07-20 |
SA518390908B1 (ar) | 2021-07-12 |
CN107921395A (zh) | 2018-04-17 |
US20180243713A1 (en) | 2018-08-30 |
CN107921395B (zh) | 2021-06-18 |
KR102116731B1 (ko) | 2020-05-29 |
EP3313564A1 (de) | 2018-05-02 |
DE102015215662A1 (de) | 2017-02-23 |
AU2016309524B2 (en) | 2018-11-01 |
US10618021B2 (en) | 2020-04-14 |
AU2016309524A1 (en) | 2018-03-01 |
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